CN214528588U - Sewage treatment vehicle - Google Patents

Sewage treatment vehicle Download PDF

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Publication number
CN214528588U
CN214528588U CN202023138707.9U CN202023138707U CN214528588U CN 214528588 U CN214528588 U CN 214528588U CN 202023138707 U CN202023138707 U CN 202023138707U CN 214528588 U CN214528588 U CN 214528588U
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CN
China
Prior art keywords
tank
sewage treatment
sewage
sludge discharge
interlayer
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CN202023138707.9U
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Chinese (zh)
Inventor
刘建福
游炳松
刘国栋
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Fujian Yanheng Industrial Co ltd
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Fujian Yanheng Industrial Co ltd
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Priority to CN202023138707.9U priority Critical patent/CN214528588U/en
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Abstract

The utility model relates to a sewage treatment car, it is including handling the car body and setting up the carriage on handling the car body, anaerobic tank, first good oxygen pond, mud centrifuge, setting tank and reaction box have connected gradually in the carriage, the anaerobic tank is connected with sewage suction pipe way, the reaction box is connected with drainage pipe. This application has the effect that improves sewage treatment economic benefits.

Description

Sewage treatment vehicle
Technical Field
The application relates to the field of sewage treatment equipment, in particular to a sewage treatment vehicle.
Background
The sewage treatment equipment can effectively treat domestic sewage, prevents sewage and pollutants from directly flowing into a water area, and has important significance for improving ecological environment and promoting economic development.
At present, the related art generally discharges domestic sewage into a sewage treatment plant, filters and decontaminates the sewage through a sewage treatment process of the sewage treatment plant, and then discharges the sewage into an underground drainage system.
In view of the above-mentioned related technologies, the inventor believes that, for some areas where the sewage discharge is relatively non-concentrated, the sewage treatment efficiency of the sewage treatment plant is not high, and the construction of the sewage treatment plant needs a lot of manpower and material resources, so that the defect of low economic benefit exists.
SUMMERY OF THE UTILITY MODEL
In order to improve sewage treatment's economic benefits, this application provides a sewage treatment car.
The application provides a sewage treatment car adopts following technical scheme:
the utility model provides a sewage treatment car, is including handling the car body and setting up the carriage on handling the car body, anaerobic tank, first good oxygen pond, row's mud centrifuge, setting tank and reaction box have connected gradually in the carriage, the anaerobic tank is connected with sewage suction pipe way, the reaction box is connected with drainage pipe.
Through adopting above-mentioned technical scheme, most organic matters are got rid of through the anaerobism pond to sewage, and the organic matter that the rethread first good oxygen pond will not get rid of completely decomposes into the inorganic matter, arranges mud centrifuge and the separation of water in with the sewage, and the water that has separated mud gets into the further sediment of setting tank again, then gets into and carries out chemical reaction in the reaction box, further gets rid of impurity such as organic phosphorus in the sewage, obtains comparatively clean water at last and discharges from drainage pipe.
Preferably, a sludge discharge pipe is connected in the sludge discharge centrifugal machine, and a discharge port of the sludge discharge pipe is connected with a sludge discharge pump.
Through adopting above-mentioned technical scheme, the mud pump passes through the mud pipe and discharges the mud in the mud centrifuge to improve mud centrifuge's live time.
Preferably, a first filter screen is arranged at a water outlet of the sludge discharge centrifugal machine.
Through adopting above-mentioned technical scheme, can prevent that a large amount of mud from being brought into the setting tank through setting up first filter screen.
Preferably, the water outlet of the sludge discharge centrifugal machine is connected to the side wall of the lower end of the settling tank, a first interlayer is arranged in the settling tank, a plurality of settling tubes are arranged on the first interlayer at intervals and are obliquely arranged, and the water outlet of the settling tank is arranged above the first interlayer.
Through adopting above-mentioned technical scheme, through setting up a plurality of sedimentation pipes, when sewage got into the sedimentation pipe, granule in the sewage can be faster deposit get off, because the sedimentation pipe slope sets up, the granule of sediment is difficult for adhering to on the lateral wall of sedimentation pipe, and the granule of sediment can the landing to the setting tank bottom, and the sewage that has deposited at last flows to the reaction box in from the delivery port flow direction of setting tank top.
Preferably, a second interlayer is arranged between the water inlet of the settling tank and the first interlayer, and a plurality of buffer holes are arranged on the second interlayer at intervals.
Through adopting above-mentioned technical scheme, through setting up a plurality of buffer holes, sewage can obtain the buffering before getting into the sedimentation pipe, and the sediment of sewage is more steady.
Preferably, a second filter screen is arranged in the anaerobic tank.
Through adopting above-mentioned technical scheme, through setting up the second filter screen, when sewage just got into the anaerobism pond, suspended solid matter and the great solid-state material of volume in the sewage all can be filtered.
Preferably, a second aerobic tank is further arranged in the carriage, and the second aerobic tank is arranged between the first aerobic tank and the sludge discharge centrifugal machine.
By adopting the technical scheme, the organic matters are decomposed by the first aerobic tank under higher organic load, the organic matters in the second aerobic tank are less, and the ammonia nitrogen in the sewage can be further degraded by the second aerobic tank under lower organic load.
Preferably, air supply pipes are arranged in the first aerobic tank and the second aerobic tank, and fans for supplying air to the two air supply pipes are arranged in the carriage.
Through adopting above-mentioned technical scheme, through setting up fan and air supply pipe, the air supply pipe is constantly the oxygen suppliment in to first good oxygen pond and the good oxygen pond of second to make the aquatic dissolved oxygen volume in first good oxygen pond and the good oxygen pond of second maintain at normal level, make the better growth of aerobic microorganism breed, and then better decompose the organic matter.
Preferably, a stirrer is arranged in the reaction box.
Through adopting above-mentioned technical scheme, can make the more thorough of the sewage reaction in the reaction box through setting up the agitator.
In summary, the present application includes at least one of the following beneficial technical effects:
(1) most organic matters in the sewage are removed through an anaerobic tank, the incompletely removed organic matters are decomposed into inorganic matters through a first aerobic tank, sludge and water in the sewage are separated through a sludge discharge centrifugal machine, the water after sludge separation enters a settling tank for further settling, then enters a reaction tank for chemical reaction, impurities such as organic phosphorus in the sewage are further removed, and finally the obtained relatively clean water is discharged from a drainage pipeline;
(2) through the arrangement of the plurality of sedimentation pipes, when sewage enters the sedimentation pipes, particles in the sewage can be quickly settled, the settled particles are not easy to attach to the side walls of the sedimentation pipes due to the inclined arrangement of the sedimentation pipes, the settled particles can slide to the bottom of the sedimentation tank, and finally, the settled sewage flows into the reaction tank from a water outlet above the sedimentation tank;
(3) the first aerobic tank decomposes organic matters under higher organic load, the second aerobic tank has less organic matters, and the second aerobic tank can further degrade ammonia nitrogen in sewage under lower organic load.
Drawings
FIG. 1 is a schematic structural view of a sewage treatment vehicle according to an embodiment of the present application;
fig. 2 is an enlarged view at a in fig. 1.
Description of reference numerals: 1. a processing vehicle body; 2. a carriage; 3. an anaerobic tank; 4. a first aerobic tank; 5. a second aerobic tank; 6. a sludge discharge centrifuge; 7. a settling tank; 8. a reaction box; 9. a sewage suction pipeline; 10. a water pump; 11. a water discharge pipeline; 12. a second filter screen; 13. a gas supply pipe; 14. an air outlet; 15. a fan; 16. a sludge discharge pipe; 17. a sludge discharge pump; 18. a first filter screen; 19. a first barrier layer; 20. a settling tube; 21. a second barrier layer; 22. a buffer hole; 23. a stirrer.
Detailed Description
The present application is described in further detail below with reference to figures 1-2.
The embodiment of the application discloses a sewage treatment vehicle. Referring to fig. 1, the sewage treatment car is including handling car body 1 and the carriage 2 of setting in handling car body 1 rear end, be provided with sewage treatment system in the carriage 2, sewage treatment system includes anaerobism pond 3 by 2 front ends in carriage to 2 rear ends in carriage in proper order, first good oxygen pond 4, arrange mud centrifuge 6, setting tank 7 and reaction box 8, anaerobism pond 3, first good oxygen pond 4, the good oxygen pond 5 of second, arrange mud centrifuge 6, all through the pipe connection between setting tank 7 and the reaction box 8, anaerobism pond 3 is connected with sewage suction pipe 9, sewage suction pipe 9 one end has suction pump 10, reaction box 8 is connected with drainage pipe 11. Wherein the sludge discharge centrifuge 6 is a small-sized centrifuge; activated sludge is filled in the anaerobic tank 3, the first aerobic tank 4 and the second aerobic tank 5; the reaction chamber 8 is filled with a reactant.
The sewage suction pipeline 9 pumps the sewage into the anaerobic tank 3 through the water suction pump 10, and the anaerobic bacteria in the anaerobic tank 3 release phosphorus in the sewage through a hydrolysis stage, an acidification stage and a methanation stage, and simultaneously ammoniate partial organic matters. The sewage in the anaerobic tank 3 passes through the first aerobic tank 4, and the microorganisms in the first aerobic tank 4 decompose the organic matters in the sewage into inorganic matters and degrade ammonia nitrogen in the sewage. Because the organic load of the first aerobic tank 4 is higher, a large amount of organic matters need to be decomposed, and the ammonia nitrogen removal effect is poor, the water in the first aerobic tank 4 enters the second aerobic tank 5, the organic load of the second aerobic tank 5 is smaller, and ammonia nitrogen in the water can be further degraded.
The sewage in the second aerobic pool 5 flows into a sludge discharge centrifuge 6, the sludge discharge centrifuge 6 generates centrifugal force through rapid rotation to separate sludge from water in the water, the water after separating the sludge enters a settling tank 7 for further settling and then enters a reaction tank 8, a reactant in the reaction tank 8 reacts with organic phosphorus dissolved in the sewage to generate metal phosphate which is insoluble in water, and finally, cleaner water is obtained and discharged through a drainage pipeline.
In this example, the reactant is a ferric sulfate reagent, and in another embodiment, the reactant may be a metal salt such as quicklime or aluminum sulfate, and forms a metal phosphate that is hardly soluble in water by reacting with organic phosphorus in the sewage.
The upper end of the anaerobic tank 3 is provided with a second filter screen 12, and when sewage just enters the sewage treatment system, the filter screen in the anaerobic tank 3 can filter suspended matters and solid matters with larger volume in the sewage.
The bottom of the first aerobic pool 4 and the bottom of the second aerobic pool 5 are both horizontally provided with an air supply pipe 13, the air supply pipe 13 is provided with a plurality of air outlets 14 at intervals along the length direction, one end of each air supply pipe 13 close to each other extends to the outer sides of the first aerobic pool 4 and the second aerobic pool 5, the bottom of the carriage 2 is provided with a fan 15, and the fan 15 supplies air to the two air supply pipes 13. The fan 15 continuously supplies oxygen to the first aerobic tank 4 and the second aerobic tank 5 through the two air supply pipes 13, and the amount of the water-soluble oxygen in the first aerobic tank 4 and the second aerobic tank 5 can be maintained at about 3-5mg/L, so that the device is suitable for the propagation of microorganisms, and can decompose organic matters in sewage.
The mud discharging centrifugal machine 6 is internally connected with a mud discharging pipe 16, one end of the mud discharging pipe 16, which extends out of the outer side of the mud discharging centrifugal machine 6, is connected with a mud discharging pump 17, and the mud discharging pump 17 pumps out the mud in the mud discharging centrifugal machine 6 through the mud discharging pipe 16, so that the mud discharging centrifugal machine 6 is prevented from being blocked by the mud. The water outlet of the sludge discharge centrifuge 6 is provided with a first filter screen 18, and the first filter screen 18 can prevent a large amount of sludge from flowing into the settling tank 7.
Referring to fig. 2, the water outlet of the sludge discharge centrifuge 6 is connected to the lower end side wall of the settling tank 7, a first interlayer 19 is arranged at the middle position inside the settling tank 7, the water outlet of the settling tank 7 is arranged on the side wall of the settling tank 7 above the first interlayer 19, a plurality of settling tubes 20 are arranged on the first interlayer 19 at intervals, the settling tubes 20 are communicated with the upper end and the lower end inside the settling tank 7, and the settling tubes 20 are obliquely arranged towards the water outlet. When water in the mud centrifuge 6 gets into the setting tank 7, sewage is excessive upwards through a plurality of sedimentation pipes 20, because the setting of sedimentation pipe 20 slope, when consequently sewage gets into the setting pipe 20, the granule in the sewage is very fast to settle down, and the granule is difficult to be attached to on the inner wall of setting pipe 20, and the setting tank 7 bottom is gone up to most granule can be followed to the sedimentation pipe 20 landing.
A second interlayer 21 is arranged between the water inlet of the settling tank 7 and the first interlayer 19, and a plurality of buffer holes 22 are arranged on the second interlayer 21 at intervals. When the sewage in the first centrifugal machine flows to the settling tank 7, the sewage can be buffered by the buffer hole 22, the sewage between the first interlayer 19 and the second interlayer 21 overflows to the settling pipe 20 more stably, and particles in the sewage can be better settled.
Referring to fig. 1, the stirrer 23 is disposed at the upper end of the reaction box 8, and when sewage in the settling tank 7 enters the reaction box 8 from the upper end side wall of the reaction box 8, the sewage can be fully reacted with the reactant in the reaction box 8 through continuous stirring of the stirrer 23, so that organic phosphorus in the sewage can be removed more cleanly, and finally, the sewage is discharged from a drainage pipeline.
The implementation principle of the sewage treatment vehicle in the embodiment of the application is as follows: set gradually anaerobism pond 3 in carriage 2, first good oxygen pond 4, the good oxygen pond of second 5, arrange mud centrifuge 6, setting tank 7 and reaction box 8, the suspended solid, solid-state material and the organic matter in anaerobism pond 3, the good oxygen pond of first 4 and the good oxygen pond of second 5 removal sewage, arrange mud centrifuge 6 and setting tank 7 and remove the mud in the sewage, remove the organic phosphorus in the sewage through reaction box 8 at last to obtain comparatively clean water.
The above embodiments are preferred embodiments of the present application, and the protection scope of the present application is not limited by the above embodiments, so: all equivalent changes made according to the structure, shape and principle of the present application shall be covered by the protection scope of the present application.

Claims (9)

1. The utility model provides a sewage treatment car which characterized in that: including handling car body (1) and setting carriage (2) on handling car body (1), anaerobic tank (3), first good oxygen pond (4), row's mud centrifuge (6), setting tank (7) and reaction box (8) have connected gradually in carriage (2), anaerobic tank (3) are connected with sewage suction pipe way (9), reaction box (8) are connected with drainage pipe (11).
2. The sewage treatment vehicle of claim 1, wherein: a sludge discharge pipe (16) is connected in the sludge discharge centrifugal machine (6), and a sludge discharge port of the sludge discharge pipe (16) is connected with a sludge discharge pump (17).
3. The sewage treatment vehicle of claim 2, wherein: and a first filter screen (18) is arranged at a water outlet of the sludge discharge centrifugal machine (6).
4. The sewage treatment vehicle of claim 1, wherein: the water outlet of the sludge discharge centrifugal machine (6) is connected to the side wall of the lower end of the settling tank (7), a first interlayer (19) is arranged in the settling tank (7), a plurality of settling tubes (20) are arranged on the first interlayer (19) at intervals and are arranged in a plurality of inclined modes, and the water outlet of the settling tank (7) is arranged above the first interlayer (19).
5. The sewage treatment vehicle of claim 4, wherein: a second interlayer (21) is arranged between the water inlet of the settling tank (7) and the first interlayer (19), and a plurality of buffer holes (22) are arranged on the second interlayer (21) at intervals.
6. The sewage treatment vehicle of claim 1, wherein: and a second filter screen (12) is arranged in the anaerobic tank (3).
7. The sewage treatment vehicle of claim 1, wherein: a second aerobic tank (5) is also arranged in the carriage (2), and the second aerobic tank (5) is arranged between the first aerobic tank (4) and the sludge discharge centrifuge (6).
8. The sewage treatment truck of claim 7, wherein: air supply pipes (13) are arranged in the first aerobic tank (4) and the second aerobic tank (5), and fans (15) for supplying air to the two air supply pipes (13) are arranged in the carriage (2).
9. The sewage treatment vehicle of claim 1, wherein: a stirrer (23) is arranged in the reaction box (8).
CN202023138707.9U 2020-12-23 2020-12-23 Sewage treatment vehicle Active CN214528588U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202023138707.9U CN214528588U (en) 2020-12-23 2020-12-23 Sewage treatment vehicle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202023138707.9U CN214528588U (en) 2020-12-23 2020-12-23 Sewage treatment vehicle

Publications (1)

Publication Number Publication Date
CN214528588U true CN214528588U (en) 2021-10-29

Family

ID=78295191

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202023138707.9U Active CN214528588U (en) 2020-12-23 2020-12-23 Sewage treatment vehicle

Country Status (1)

Country Link
CN (1) CN214528588U (en)

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GR01 Patent grant
CB03 Change of inventor or designer information
CB03 Change of inventor or designer information

Inventor after: Liu Yushan

Inventor after: Liu Honghui

Inventor after: Liu Guodong

Inventor before: Liu Jianfu

Inventor before: You Bingsong

Inventor before: Liu Guodong